US6166275AExpiredUtility
Fluorination process
Priority: Nov 18, 1997Filed: Sep 17, 1999Granted: Dec 26, 2000
Est. expiryNov 18, 2017(expired)· nominal 20-yr term from priority
Y02P20/582C07C 17/383C07C 17/206C07C 17/20
33
PatentIndex Score
7
Cited by
8
References
7
Claims
Abstract
A liquid phase fluorination process for producing difluoromethane without corrosion is provided. In the process of this invention, methylene chloride and hydrogen fluoride are reacted in a reactor made of fluorinated polymer to produce a reaction product while a vaporized and superheated recycle stream of process reactants is fed into the reactor.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A process comprising the steps of: (a) reacting reactants comprising methylene chloride and hydrogen fluoride in the presence of an effective amount of a fluorination catalyst and in a reactor made of a fluorinated polymer to produce a reaction product; and (b) distilling the reaction product in a first distillation column to produce a first column bottoms product that is recycled to the reactor and a first column overhead product comprising hydrogen chloride, difluoromethane, monochloromonofluoromethane, methylene chloride, and hydrogen fluoride; (c) distilling the first column overhead product in a second distillation column to produce a second column bottoms product comprising monochloromonofluoromethane, methylene chloride, and hydrogen fluoride and a second column overhead product comprising difluoromethane and hydrogen chloride; (d) vaporizing and superheating the second column bottoms product; and (e) recycling the vaporized and superheated second column bottoms product to the reactor.
2. The process of claim 1 wherein the first and second column bottoms products are superheated to a temperature of about 100 to about 200° C. before being recycled to the reactor.
3. A process comprising the steps of: (a) reacting reactants comprising methylene chloride and hydrogen fluoride in the presence of an effective amount of a fluorination catalyst and in a reactor made of a fluorinated polymer to produce a reaction product; and (b) distilling the reaction product in a first distillation column to produce a first column bottoms product that is recycled to the reactor and a first column overhead product comprising hydrogen chloride, difluoromethane, monochloromonofluoromethane, methylene chloride and hydrogen fluoride; (c) distilling the first column overhead in a second distillation column to produce a second column bottoms product comprising difluoromethane, monochloromonofluoromethane, methylene chloride, and hydrogen fluoride and a second column overhead product comprising hydrogen chloride; (d) distilling the second column bottoms product in a third distillation column to produce a third column bottoms product comprising monochloromonofluoromethane, methylene chloride, and hydrogen fluoride and a third column overhead product comprising difluoromethane; (e) vaporizing and superheating the third column bottoms product; and (f) recycling the vaporized and superheated third column bottoms product to the reactor.
4. The process of claim 3 wherein the first, second and third column bottoms products are superheated to a temperature of about 100 to 200° C. before being recycled to the reactor.
5. A process comprising the steps of: (a) reacting reactants comprising methylene chloride and hydrogen fluoride in a reactor made of a fluorinated polymer in the presence of a fluorination catalyst to produce a reaction product; (b) distilling the reaction product in a distillation column to produce a column bottoms product comprising hydrogen fluoride, methylene chloride and monochloromonofluoromethane and a column overhead product comprising hydrogen chloride, difluoromethane, monochloromonofluoromethane, methylene chloride, and hydrogen fluoride; (c) partially vaporizing the column bottoms product to produce a vapor portion and liquid portion; (d) superheating the vapor portion; and (e) recycling the superheated vapor portion and the liquid portion to the reactor.
6. A process comprising the steps of: (a) reacting reactants comprising methylene chloride and hydrogen fluoride in a reactor made of a fluorinated polymer in the presence of a fluorination catalyst to produce a reaction product, (b) distilling the reaction product in a distillation column to produce a column bottoms product comprising hydrogen fluoride, methylene chloride and monochloromonofluoromethane and a column column overhead product comprising hydrogen chloride, difluoromethane, monochloromonofluoromethane, methylene chloride, and hydrogen fluoride; (c) withdrawing a liquid sidestream from an intermediate part of the distillation column; (d) vaporizing and superheating the liquid sidestream; and (e) recycling the vaporized and superheated liquid sidestream to the reactor.
7. The process of claim 6 wherein the liquid sidestream is partially vaporized to produce a vapor portion and a liquid portion; the vapor portion is superheated; and the superheated vapor portion and the liquid portion are recycled to the reactor.Cited by (0)
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